| HS Code | 532035 |
| Density | 0.90 g/cm³ |
| Melt Flow Rate | 11 g/10 min (230°C/2.16 kg) |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Yield | 11% |
| Flexural Modulus | 1400 MPa |
| Izod Impact Strength Notched 23 C | 3.5 kJ/m² |
| Heat Deflection Temperature Hdt 0 45 Mpa | 100°C |
| Vicat Softening Point | 155°C |
| Rockwell Hardness | R 100 |
| Melting Point | 160°C |
As an accredited Polypropylene PP K1011 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polypropylene PP K1011 is packaged in 25 kg woven plastic bags with inner liners, palletized and wrapped for safe transport. |
| Container Loading (20′ FCL) | Polypropylene PP K1011 is loaded in 25kg woven bags onto pallets, securely stowed in a 20′ FCL, about 20 tons per container. |
| Shipping | Polypropylene PP K1011 is shipped as non-hazardous granules in 25 kg bags, jumbo bags, or bulk containers. Transport by truck, rail, or sea is standard. Keep packaging dry, avoid high heat and direct sunlight, and store in a ventilated area away from ignition sources. No dangerous goods classification required. |
| Storage | Store Polypropylene PP K1011 in a cool, dry, well-ventilated area, away from direct sunlight, heat, and open flames. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid storage near strong oxidizing agents. Maintain warehouse temperatures below 40°C. Proper storage preserves material properties and prevents degradation. |
| Shelf Life | Store unopened in cool, dry, shaded conditions. Shelf life is typically 2 years from manufacture when protected from moisture and heat. |
K1011 enters thin-gauge packaging not as a random copolymer but as a homopolymer with a nominal melt mass-flow rate of 15 g/10 min measured at 230 °C under a 2.16 kg piston load according to ISO 1133-1:2022. That melt-flow position permits filling of dairy tubs and deli containers at wall sections from 0.45 mm to 0.80 mm without flash, provided the flow-length-to-thickness ratio is maintained below approximately 220:1. Higher ratios force melt temperature upward and create gate blush, short shots, or dimensional ovality. Food-contact status rests on FDA 21 CFR 177.1520(c) 1.1 for polypropylene homopolymer and on EU Regulation (EU) No 10/2011 Annex I. Overall migration into food simulants must not exceed 10 mg/dm² under the selected simulant and time-temperature condition. Pigment and nucleator packages must also be positive-listed for the intended simulant.
In thin-wall production, the dry blend is seldom neat resin. Typical additions are a PP-carrier white masterbatch at 2.0-3.0 wt%, a nucleating agent masterbatch at 0.5-1.0 wt% to raise crystallization temperature and stabilise gloss, and a slip/antiblock masterbatch at 0.3-0.8 wt% where stacked containers must release without scuffing. On a 200-350 metric ton hydraulic toggle injection moulding machine with a 22:1 L/D general-purpose PP screw and a compression ratio of 2.5:1, melt temperature is held at 220-245 °C and mould temperature at 15-30 °C to shorten cooling time. Injection velocity is set between 120 mm/s and 220 mm/s for multi-cavity hot-runner tools. Hold pressure is typically 35-55 MPa hydraulic, with hold-time consumption below 1.5 s for a 0.60 mm wall. Total cycle time on a four-cavity dairy cup tool commonly falls between 6.5 s and 8.5 s. Short shots appear when cavity filling pressure exceeds available clamp tonnage or when flow length crosses 250:1. Gate blush and jetting arise when cold slug wells in the hot-runner drop have insufficient diameter. Differential cooling between the gate and rim produces ovality above 0.3 mm on a 500 mL tub if hold pressure decays before gate freeze. The resulting end products are injection-moulded dairy cups, takeaway tubs, and stackable deli containers. Microwavability in these items is limited by the homopolymer’s heat deflection temperature under load of approximately 100 °C at 0.45 MPa; boiling-water exposure above 100 °C causes distortion unless the part is specifically designed with reinforcing rims and lidding shoulders.
For closure applications, the decision boundary is carbonation. K1011 is used for non-carbonated flip-top caps, sports-cap bases, and loose-pack closures for dry products. Carbonated soft-drink closures tend to shift to random copolymer polypropylene because the homopolymer’s notched Izod impact at room temperature sits near 2.7 kJ/m² under ISO 180/1A. Retained stress at the tamper-evident bridge can propagate a crack when the package is dropped from 0.5 m after cold filling. For food-contact caps, the same FDA 21 CFR 177.1520(c) status applies. Organoleptic requirements under EU Regulation (EU) No 10/2011 Article 3 require that migrating substances must not cause unacceptable modification of taste or odour. In practice, erucamide slip is limited to 0.10-0.25 wt% because higher loading reduces coefficient of friction but also increases organoleptic transfer to dry foods. If a foamed LDPE induction seal liner is used, the PP cap body remains compatible with the PE-based sealing layer, while a PET-based liner requires a separate compatibility check.
High-cavitation moulds for caps use a 32-cavity or 48-cavity hot-runner system with valve gate diameter 0.5-0.8 mm. Melt temperature is kept lower than in thin-wall packaging, 215-235 °C, to prevent flashing at the sealing plug. Mould temperature is 25-40 °C. Demoulding is assisted by a stripper plate and gentle unscrewing for internal threads rather than forced ejection. Cycle time for a 2.0 g sports-cap base on a 72-cavity tool is typically 4.5-6.0 s when using a polypropylene homopolymer with MFR near 15 g/10 min. Production output is directed to dry product closures, personal-care flip-tops, and detergent cap bodies where continuous stress from carbonation is absent.
Internal refrigerator shelf brackets, washing-machine dispenser bodies, and small appliance feet are moulded from K1011 when flexural modulus governs wall-section decisions and impact is a secondary load. The homopolymer’s flexural modulus is nominally 1370 MPa under ISO 178 for a 3.2 mm moulded specimen, which allows brackets to be thinner than a lower-stiffness random copolymer. RoHS compliance is certified by supplier declaration under Directive 2011/65/EU and amendment (EU) 2015/863; REACH SVHC content for the four phthalates and heavy metals is checked through XRF screening at incoming quality control. These parts are typically moulded in natural or black. Black specimens incorporate 2.0 wt% carbon black masterbatch to stabilise colour and provide modest UV weathering. No impact modifier is added; adding 5-10 wt% ethylene-octene copolymer would raise room-temperature impact but would lower flexural modulus by 100-150 MPa and increase creep.
Wall thickness is kept between 1.5 mm and 3.0 mm to avoid sink marks over ribs. Melt temperature is 220-240 °C, mould temperature 30-45 °C, and holding pressure 45-65 MPa hydraulic. Weld lines form around fixing holes and are the primary fracture initiation sites because homopolymer weld-line strength can be 40-60% of the bulk tensile yield strength. End products include refrigerator shelf supports, detergent drawer bodies, and appliance levelling feet. Service is confined to ambient indoor exposure; sub-zero temperature is excluded because impact falls sharply.
Industrial pails and heavy-duty crates produced from K1011 are designed for ambient distribution, not frozen storage. The material’s notched Izod impact under ISO 180/1A is approximately 2.5-3.0 kJ/m² at 23 °C, but homopolymer polypropylene undergoes a ductile-to-brittle transition as service temperature approaches the glass transition region near -10 °C to 0 °C. At -20 °C, measured notched Izod values can fall below 1.5 kJ/m², which is insufficient for drop tests of full pails from 1.2 m. This limitation is observed on palletised shipment lines where filled pails are stored in cold warehouses. Pails intended for dangerous goods require UN certification under ADR/RID/IMDG as packaging group II or III depending on product and specific gravity. The moulded pail is tested for stacking load, leakproofness, and drop height. A homopolymer PP pail passes ambient drop tests at 20 °C when wall thickness is 2.0-2.5 mm, but the same design frequently fails at -18 °C unless an impact modifier is introduced.
To offset UV degradation in outdoor crate service, a HALS stabiliser at 0.15-0.30 wt% and carbon black at 1.5-2.5 wt% are used. Compounding is performed by direct masterbatch let-down into the injection machine feed throat; dispersion is evaluated by carbon black particle agglomerate count on a polished microtome section under 200× optical microscopy. Processing runs on a 500-800 ton injection press with a 20:1-24:1 L/D screw. Melt temperature is held at 225-250 °C. Mould temperature is deliberately low, 15-25 °C, to increase cooling rate and reduce cycle time on a 15 L pail tool. Holding pressure is high, 60-80 MPa hydraulic, with holding time extended to 8-12 s to ensure gate freeze and avoid sink marks at the handle lugs. Typical end products are non-food industrial pails, paint containers, and returnable agricultural crates. Heavy crate lids that must resist top-load compression above 150 kg for 48 h are normally cross-braced or ribbed to avoid buckling because homopolymer PP creep modulus is lower than reinforced grades.
For dry electrical enclosures, terminal blocks, and non-flame-rated consumer switch housings, K1011 is used only in circuits where the final part can comply with UL 94 at the level of HB and does not require V-2 or V-0. Homopolymer PP with a wall thickness of 1.5 mm is generally assigned to HB in the UL yellow-card system; a V-2 rating requires a halogenated or halogen-free flame-retardant package that changes melt flow and may cause mould staining. Electrical insulation capability is anchored to volume resistivity above 1.0 × 10¹⁶ Ω·cm under IEC 62631-3-1 and surface resistivity above 1.0 × 10¹⁵ Ω. Antistatic or carbon black modifications reduce these values by orders of magnitude. For K1011 specifically, published extractables data at food simulant time-temperature conditions is limited; converters therefore maintain internal migration libraries rather than relying on grade-specific statements.
| Sector | Standard | K1011 condition |
|---|---|---|
| Food-contact packaging | FDA 21 CFR 177.1520(c); EU 10/2011 Annex I | Overall migration limit 10 mg/dm²; organoleptic compliance required |
| Cosmetic and closure packaging | EU (EC) No 1223/2009 packaging migration via supplier declaration | Slip loading 0.10-0.25 wt% to limit extractables |
| Dry electrical enclosure | IEC 60695-2-11; UL 94 | HB only unless FR-modified; not for energised parts |
| Laboratory consumable | ISO 10993-5; USP Chapter 87 | Unfilled homopolymer is not inherently certified; batch testing is required |
Unfilled K1011 is preferred because fillers lower volume resistivity and complicate bio-inertness. For diagnostic housings, a light-stable colour masterbatch is used at 0.5-1.5 wt%. External mould-release sprays are avoided because release-agent transfer can interfere with adhesive labels and ISO 10993-5 cytotoxicity endpoints. Processing requires lower screw speed, 50-100 rpm, and back pressure 0.5-1.0 MPa to avoid shear heating. Melt temperature is 210-230 °C; mould temperature is 25-40 °C. Drying at 80 °C for 2-3 h is implemented when resin cartons have been opened longer than 24 h in relative humidity above 60%. End products include terminal covers, non-energised switch covers, centrifuge tube stands, and diagnostic instrument covers. Any part intended for direct patient contact is qualified under ISO 10993-1 after the moulder demonstrates batch-to-batch consistency in residual catalyst and additive extraction.
Office storage shells, clip-together stationery articles, and consumer organising trays are shallow processing zones for K1011. The resin’s melt flow permits thin visible shells with gloss, but no critical compliance burden exists beyond REACH SVHC screening under REGULATION (EC) No 1907/2006 and heavy metals below EN 71-3 migration limits where the article is sold as a toy. Melt temperature is 220 °C, mould temperature 25 °C, and fast injection is used; no post-treatment is required. Output includes drawer organisers, binder shells, and potting trays intended for indoor use only.
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Polypropylene PP K1011 is an unfilled polypropylene homopolymer supplied as pelletized resin with a nominal melt mass-flow rate of 11 g/10 min when determined according to ISO 1133-1:2022 at 230 °C under 2.16 kg. The manufacturer-specific K1011 designation is not an ISO 1873 classification; it is a trade grade identifier. The product occupies the moderate-flow segment between low-melt-flow extrusion homopolymers and high-flow thin-wall injection grades. It is selected for rigid packaging closures, caps with tamper-evident bands, small appliance housings, hangers, pails, containers, and general technical parts produced by injection moulding with nominal wall sections from 1.0 mm to 2.5 mm.
The resin is typically stabilized with a phenolic antioxidant and a phosphite processing stabilizer, with an acid scavenger to neutralise residual catalyst acidity. It is not an inherently UV-stabilized grade. Unmodified K1011 homopolymer can be pigmented in the melt but remains opaque in thick sections; it is not intended for transparent contact-clarity or freezer-impact applications. For parts requiring prolonged outdoor exposure, a separate additive package is required.
Lot release specifications normally control melt mass-flow rate within ±1.0 g/10 min around nominal, together with tensile yield stress, flexural modulus, density, ash content, and impact behaviour. Secondary characterisation follows ISO 527-2:2012, ISO 178:2019, ISO 1183-1:2019, ISO 179-1:2010, and ISO 75-2:2013. The producer’s certificate of analysis is the only valid source of lot-specific values; Table 1 presents the expected screening range for unfilled polypropylene homopolymer of the MFR 11 class, not a specification for a specific production lot.
| Property | Method | Representative range | Unit |
|---|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 11 (nominal) | g/10 min |
| Density | ISO 1183-1:2019 | 0.900–0.910 | g/cm³ |
| Tensile yield stress | ISO 527-2:2012 | 34–37 | MPa |
| Flexural modulus | ISO 178:2019 | 1400–1600 | MPa |
| Notched Izod impact, 23 °C | ISO 180:2019 | 2.5–4.5 | kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013 | 95–105 | °C |
| Vicat softening temperature, A/50 | ISO 306:2022 | 153–157 | °C |
| Mould shrinkage allowance | ISO 294-4:2018 | 1.0–1.8 | % |
Because polypropylene is non-hydroscopic, desiccant drying is not required under normal indoor storage at relative humidity below 60%. If condensate from cold warehouse transfer or high-humidity storage is present, a desiccant dryer at 80 °C for 2–4 h with a dew point below -30 °C removes surface moisture. Drying above 90 °C risks pellet agglomeration.
The 11 g/10 min MFR creates a measurable flow-length limit. In spiral-flow screening at 230 °C melt temperature, 2 mm test-channel depth and 1000 bar peak pressure, MFR 11 homopolymer resins typically fill 70–100 cm. Published spiral-flow data for the specific K1011 grade are limited; processor-generated curves are required for moulds with flow-length-to-wall-thickness ratios above 150:1 or for features below 0.6 mm.
Thermal load is governed by residence time and the stabilizer package. On a 150-tonne hydraulic injection moulding machine with a 22:1 L/D general-purpose screw and compression ratio 2.5:1, stable operation occurs at melt temperatures of 220–245 °C. At melt temperatures below 210 °C, viscosity rises enough to cause short shots in 0.6 mm cap ribs; at melt temperatures above 260 °C and residence times exceeding 10 min, visible splay and yellowing appear as antioxidant depletion and molecular-weight degradation begin. Shot weight should use 60–80% of barrel capacity to avoid excessive residence.
Melt temperature at the nozzle should be checked with an air-shot probe at the start of each production run. A stable melt temperature of 230 °C does not guarantee uniform melt at the nozzle if the screw recovery speed is excessively high. Screw speed is normally limited to 80–120 rpm on a 35 mm diameter screw; higher speeds generate shear-induced melt-temperature overshoots of 10–15 °C, contributing to gate blush and part weight variation.
Barrel profile: feed 200–210 °C, compression 210–230 °C, metering 220–240 °C, nozzle 220–235 °C. Mould surface temperature is normally 30–50 °C. Higher mould temperatures reduce post-mould shrinkage and orientational stress but increase cycle time; lower mould temperatures below 20 °C can produce sink marks opposite ribs and bosses.
During thin-wall cap moulding in a 16-cavity hot-runner tool, fill time of 1.0–1.8 s at transfer pressure of 800–1200 bar hydraulic produced complete filling without jetting. Pack pressure of 40–60% of peak injection pressure applied for 4–7 s stabilised part mass. Gate velocity should be limited to avoid jetting; in tests on 0.9 mm twin-gated parts, gate velocities above 400 mm/s produced a visible worm-like gate blush. Hold pressure decay should be gradual to avoid underpacking at the hot-runner drool.
Application practice in rigid closures shows a quantifiable pressure difference between K1011 and a high-flow MFR 35 g/10 min grade. In the same 28 mm tamper-evident cap tool with 0.9 mm skirt wall, the high-flow grade fills at approximately 12% lower injection pressure, but gate-area sink and dimensional covariance increase because of earlier gate freeze and reduced packing efficiency. For 1.8 mm appliance brackets, K1011 yields lower warpage than MFR 35 homopolymer because lower melt flow reduces molecular orientation anisotropy during packing. Parts requiring freezer-drop impact below -20 °C should not be moulded from unfilled K1011; notched Izod impact drops sharply once the material is below its glass transition of approximately -10 °C to 0 °C.
For opaque household containers and caps exposed to short-term hot-fill at 90 °C for up to 2 h, K1011 maintains dimensional integrity when the part is supported. Unsupported thin-wall sections distort at temperatures approaching the 0.45 MPa heat deflection temperature. For continuous service above 100 °C, PP homopolymer undergoes thermo-oxidative degradation and creep; K1011 should not be specified without a long-term oxidative stabilizer package and design validation.
In practice, PP K1011 is let down with masterbatch at 2–4 wt% unless a pre-compounded product is specified. For colour-critical closures, a carrier resin matched to MFR 11 is preferred because high-MFR carrier resins can cause local viscosity differences and colour streaks. If regrind is used, the recommended proportion is below 20% by weight for dimensional consistency in thin-wall parts. Higher regrind fractions reduce melt viscosity slightly due to molecular weight reduction and may require a 5–10 °C reduction in melt temperature.
PP K1011 is not a direct substitute for impact copolymer in parts governed by cold-impact test standards. Table 2 compares class-typical values. Impact copolymers attain notched Izod values of 5–10 kJ/m² at -20 °C, whereas unfilled MFR 11 homopolymers typically remain below 3 kJ/m² at -20 °C when tested to ISO 180:2019. In exchange, the homopolymer provides flexural modulus values 200–400 MPa higher than a typical impact copolymer and better creep resistance at 23 °C.
Transparency requirements also exclude unfilled K1011 from clear contact-clarity applications. The homopolymer class exhibits haze above 30% at 2 mm plaque thickness under ASTM D1003-21. Clarified random copolymers with ethylene content 2–4 wt% and sorbitol-based nucleators provide lower haze, but their flexural modulus is typically 200–400 MPa lower and their heat deflection temperature is 5–10 °C lower.
| Property | PP K1011 (MFR 11 g/10 min) | High-flow PP homopolymer (MFR 35 g/10 min) | PP impact copolymer (MFR 8 g/10 min) |
|---|---|---|---|
| Melt mass-flow rate | 11 g/10 min | 35 g/10 min | 8 g/10 min |
| Tensile yield stress | 34–37 MPa | 33–36 MPa | 25–28 MPa |
| Flexural modulus | 1400–1600 MPa | 1450–1700 MPa | 1100–1300 MPa |
| Notched Izod, 23 °C | 2.5–4.5 kJ/m² | 2.0–3.0 kJ/m² | 10–20 kJ/m² |
| Notched Izod, -20 °C | 1.5–3.0 kJ/m² | 1.0–2.0 kJ/m² | 5–10 kJ/m² |
| Heat deflection temperature, 0.45 MPa | 95–105 °C | 90–100 °C | 85–95 °C |
Values in Table 2 are class-typical screening data for unfilled PP homopolymer and impact copolymer; they are not lot-specific certificates and should not replace material data sheets. The differences in Table 2 are most visible in application-level testing. In a 5 L pail with wall thickness 1.6 mm, replacing K1011 with an impact copolymer reduces top-load failure under cold-drop conditions but also reduces sidewall stiffness; processors often switch to an impact copolymer only after confirming that top-load warranty criteria or dimensional stability under stack load can be met with a thicker wall. In contrast, switching from K1011 to a high-flow MFR 35 homopolymer in a thin-wall container shortens fill time but can increase sink marks at the rim because the high-flow material requires different pack and gate-freeze settings.
For heat-seal applications, unfilled homopolymer has a higher seal initiation temperature than random copolymer. K1011 is therefore specified for rigid injection-moulded parts rather than monolayer heat-seal films; if sealability is required, a heat-sealable copolymer layer or an inserted liner is used. At the same MFR, a random copolymer also has lower seal initiation temperature than PP homopolymer, which is one reason K1011 is not used as a sealing layer.
Food-contact status is formulation-specific and must be confirmed on the producer’s statement of compliance. The base polypropylene homopolymer is assessed against 21 CFR 177.1520(c), item 1.1 in the United States and Regulation (EU) No 10/2011 in the European Union, with overall migration limit 10 mg/dm² for food-contact plastics. Specific migration limits for any additives, masterbatch pigments, or processing aids must be evaluated separately.
Electrical and electronic applications require supplier confirmation of conformity to Directive 2011/65/EU as amended by (EU) 2015/863, covering lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, polybrominated diphenyl ethers, and restricted phthalates. Under Regulation (EC) No 1907/2006, the resin is supplied with a safety data sheet and, on request, an SVHC declaration; the standard commercial formulation does not contain Candidate List substances above 0.1% w/w per article.
Processing hazards include combustible dust if pellets are ground or if fines accumulate. Exhaust ventilation at the die or nozzle is required to remove trace degradation products. Storage should be in unopened bags below 40 °C and away from direct UV exposure; opened bags should be resealed to exclude moisture and airborne dust.
K1011 is not compatible with long-term contact with strong oxidizing acids, chlorine-based oxidising agents, or aromatic hydrocarbons at elevated temperature. It should not be combined with pro-oxidant additives if long-term thermo-oxidative stability is required. Outdoor weatherability requires a properly dispersed hindered amine light stabilizer or carbon black at 1.0–2.0 wt% in the compound; unpigmented homopolymer will embrittle under prolonged UV exposure without such packages.